EP1289033B1 - Anode thin film for lithium secondary battery and preparation method thereof - Google Patents

Anode thin film for lithium secondary battery and preparation method thereof Download PDF

Info

Publication number
EP1289033B1
EP1289033B1 EP02000438.8A EP02000438A EP1289033B1 EP 1289033 B1 EP1289033 B1 EP 1289033B1 EP 02000438 A EP02000438 A EP 02000438A EP 1289033 B1 EP1289033 B1 EP 1289033B1
Authority
EP
European Patent Office
Prior art keywords
tin
thin film
lithium
anode
nickel
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP02000438.8A
Other languages
German (de)
French (fr)
Other versions
EP1289033A3 (en
EP1289033A2 (en
Inventor
Young-Sin Park
Joo-Yeal Oh
Sung-Man Lee
Hong-Koo Baik
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Samsung SDI Co Ltd
Original Assignee
Samsung SDI Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Samsung SDI Co Ltd filed Critical Samsung SDI Co Ltd
Publication of EP1289033A2 publication Critical patent/EP1289033A2/en
Publication of EP1289033A3 publication Critical patent/EP1289033A3/en
Application granted granted Critical
Publication of EP1289033B1 publication Critical patent/EP1289033B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/134Electrodes based on metals, Si or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1395Processes of manufacture of electrodes based on metals, Si or alloys
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C13/00Alloys based on tin
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C14/00Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material
    • C23C14/06Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material characterised by the coating material
    • C23C14/14Metallic material, boron or silicon
    • C23C14/16Metallic material, boron or silicon on metallic substrates or on substrates of boron or silicon
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C14/00Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material
    • C23C14/22Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material characterised by the process of coating
    • C23C14/24Vacuum evaporation
    • C23C14/28Vacuum evaporation by wave energy or particle radiation
    • C23C14/30Vacuum evaporation by wave energy or particle radiation by electron bombardment
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C14/00Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material
    • C23C14/22Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material characterised by the process of coating
    • C23C14/34Sputtering
    • C23C14/3407Cathode assembly for sputtering apparatus, e.g. Target
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C14/00Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material
    • C23C14/22Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material characterised by the process of coating
    • C23C14/34Sputtering
    • C23C14/3464Sputtering using more than one target
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C14/00Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material
    • C23C14/22Coating by vacuum evaporation, by sputtering or by ion implantation of the coating forming material characterised by the process of coating
    • C23C14/34Sputtering
    • C23C14/46Sputtering by ion beam produced by an external ion source
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/04Processes of manufacture in general
    • H01M4/0402Methods of deposition of the material
    • H01M4/0421Methods of deposition of the material involving vapour deposition
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/04Processes of manufacture in general
    • H01M4/0402Methods of deposition of the material
    • H01M4/0421Methods of deposition of the material involving vapour deposition
    • H01M4/0423Physical vapour deposition
    • H01M4/0426Sputtering
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/387Tin or alloys based on tin
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/02Making metallic powder or suspensions thereof using physical processes
    • B22F9/04Making metallic powder or suspensions thereof using physical processes starting from solid material, e.g. by crushing, grinding or milling
    • B22F2009/041Making metallic powder or suspensions thereof using physical processes starting from solid material, e.g. by crushing, grinding or milling by mechanical alloying, e.g. blending, milling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F2998/00Supplementary information concerning processes or compositions relating to powder metallurgy
    • B22F2998/10Processes characterised by the sequence of their steps
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0561Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of inorganic materials only
    • H01M10/0562Solid materials
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/027Negative electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0065Solid electrolytes
    • H01M2300/0068Solid electrolytes inorganic
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/40Printed batteries, e.g. thin film batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00Metal working
    • Y10T29/49Method of mechanical manufacture
    • Y10T29/49002Electrical device making
    • Y10T29/49108Electric battery cell making
    • Y10T29/49115Electric battery cell making including coating or impregnating

Definitions

  • the present invention relates to an anode thin film for lithium secondary battery and a preparation method thereof, and more particularly, to an anode thin film for a lithium secondary battery having a reduced initial irreversible capacity by using an intermetallic compound of tin (Sn) and nickel (Ni) as a material of forming an anode active material layer formed on a current collector, and having improved charging/discharging cycle characteristics by solving the problem of aggregation of tin due to intercalation/deintercalation of lithium.
  • an intermetallic compound of tin (Sn) and nickel (Ni) as a material of forming an anode active material layer formed on a current collector
  • a lithium ion battery can secure its stability and can maintain high capacitance characteristics by employing graphite as an anode-forming material.
  • graphite anode reversibly enables storage and separation of lithium through intercalation of lithium ions. Since the inserted lithium ions are not in the form of metal, factors that may adversely affect the stability of a battery, for example, growth of dendrite, can be prevented.
  • graphite anodes have only approximately 10% of an energy density of metallic lithium anodes.
  • Various anode materials including disordered carbon, nitrides or oxides, which exhibit improved capacity compared to graphite, have been proposed for overcoming the problem of small energy density.
  • Oxide-based anodes exemplified by tin oxides were proposed for the first time by Fuji Photo Film Co., Ltd., in U.S. Patent No. 5,618,640 by Y. Idota et al , and in a paper by Idota et al. entitled "Tin-Based Amorphous Oxide: A High Capacity Lithium-Ion Storage Material", Science, 276 (1997) 1395-1397 , and have approximately twice a charge/discharge capacity of graphite-based anodes and are excellent in potential characteristics compared with existing substitutes.
  • Oxide-based anodes consist of oxides of metal that can form lithium alloys, such as tin oxide (SnO or SnO 2 ), lead oxide (PbO) or silicon oxide (SiO). These oxide-based anode-forming materials serve as precursors of anode active materials. Thus, as lithium ions are diffused across the lattice of metal, oxygen ion and metal ion are separated from each other. Also, as intercalated lithium ions react with oxygen ions, separation occurs in the lattice of metal. Active materials capable of charging/discharging are substantially metals separated in the above-described manner, rather than metal oxides.
  • lithium can be stored/removed by an alloying reaction between tin and lithium.
  • oxide-based anodes consisting of oxides, e.g., tin oxide, have good cycle characteristics, compared with lithium alloys, in the following reasons.
  • a metal that can form lithium alloys e.g., tin
  • the separated metal is very small in size, the mechanical loss of an active material, due to a change in volume, can be minimized.
  • lithium oxide which is a product based on the reaction between the lithium produced simultaneously with separated metal during initial storage of lithium, and the oxygen ions, is evenly dispersed, damage of the active material due to a change in volume can be suppressed.
  • the oxide-based anode exhibits a relatively high initial irreversible capacity due to formation of lithium oxide, which is necessarily generated during the first charging/discharging cycle. Accordingly, an excess amount of a cathode active material is required, which is impediment to practical use.
  • a tin-based intermetallic compound for example, Sn 2 Fe or Cu 6 Sn 5 , consists of an intermetallic compound of a metal which does not form a lithium alloy and a metal which is reactive with lithium. Also, since the tin-based intermetallic compound does not undergo irreversible reaction, e.g., formation of lithium oxide (Li 2 O) due to diffusion of lithium ions into the lattice of metal, unlike tin oxide, initial irreversible capacity can be reduced.
  • irreversible reaction e.g., formation of lithium oxide (Li 2 O) due to diffusion of lithium ions into the lattice of metal, unlike tin oxide, initial irreversible capacity can be reduced.
  • the tin-based intermetallic compound causes aggregation of tin due to repeated intercalation/deintercalation of lithium ions, which aggravates the mechanical damage of an active material depending on a change in volume, like metallic tin, resulting in considerable deterioration of cycle characteristics.
  • the composite material include a composite material consisting of Sn 2 Fe as an active-phase material and SnFe 3 C as an inactive-phase material. While such a composite material has a fine structure, improved cycle characteristics due to addition of inactive-phase material, and an increased energy density per volume, its energy density per weight is very small, i.e., less than 200 mAh/g.
  • a lithium-tin alloy (Li 4.4 Sn) has a relatively low operating voltage with respect to a lithium electrode, i.e., 0.7 V or less, and has an energy density per unit weight of approximately 790 mAh/g, which is higher than that of a lithium-graphite compound (LiC 6 ) having an energy density of 342 mAh/g.
  • EP 1 122 802 A1 discloses a non-aqueous electrolyte secondary battery comprising a negative electrode including, as an active material, a solid solution of Li x M 1 y M 2 , where M 1 and M 2 represent specific metals, and x and y represent specific amounts of Li and M 1 , respectively.
  • a solid solution of Li x M 1 y M 2 As far as Ni and Sn are considered for M 1 and M 2 , the compositions NiSn, Ni 2 Sn, and Ni 3 Sn are proposed.
  • the solid solution typically shows an average particle size of 0.5 ⁇ m to 2.3 ⁇ m, and an average crystal grain size of 0.05 ⁇ m to 0.13 ⁇ m.
  • EP 1 043 789 A1 discloses for such negative electrode compound to have at least two phases of different composition.
  • an alloy composition NiSn is proposed to consist of an Ni 3 Sn 4 phase and an Ni 3 Sn phase as well as an Sn(2) phase.
  • the thickness of a practical negative electrode sheet is said to be about 80 ⁇ m.
  • Similar electrode compositions for a lithium ion battery with particle sizes from about 2 ⁇ m to about 30 ⁇ m and crystalline grain sizes of no more than about 20 nm are disclosed in WO 01/48840 A1 , where the particles have a microstructure including a plurality of electrochemically inactive, nanometer-sized crystalline grains separated by electrochemically active non-crystalline regions.
  • US 5,360,684 discloses an electrochemical cell having a specific lamination structure including a lithium negative electrode with a typical thickness of 20 ⁇ m and a positive electrode with a typical thickness of 40 ⁇ m.
  • an anode thin film for a lithium secondary battery includes a current collector and an anode active material layer formed thereon, wherein the anode active material layer contains an intermetallic compound of Ni 3 Sn 4 .
  • a method of preparing such anode thin film for a lithium secondary battery includes mosaic-sputtering tin (Sn) and metallic nickel (Ni), co-sputtering tin (Sn) and metallic nickel (Ni) and sputtering single target or target containing tin (Sn) and metallic nickel (Ni).
  • a method of preparing such anode thin film for a lithium secondary battery includes the steps of forming an intermetallic compound evaporation source of tin (Sn) and metallic nickel (Ni) by a mechanical alloying method and depositing the intermetallic compound evaporation source by at least selected from the group consisting of e-beam evaporation and ion beam assisted deposition (IBAD).
  • IBAD e-beam evaporation and ion beam assisted deposition
  • a lithium secondary battery employs the anode thin film.
  • the lithium secondary battery is preferably a lithium thin film battery.
  • the present invention is directed to improvement in cycle characteristics by employing an intermetallic compound of tin (Sn) and nickel (Ni) in order to solve an inherent problem of tin, that is, in order to suppress a stress due to volumetric expansion of tin, thereby improving the structural stability to improve cycle characteristics.
  • the intermetallic compound of tin (Sn) and a nickel (Ni) metal that is, Ni 3 Sn 4, the tin (Sn) being an active material of reaction with lithium (Li) and the nickel (Ni) metal not reacting with Li, does not undergo a reaction of forming a compound with Li ions diffused into a grid with oxygen ions contained in oxide, thereby almost removing the initial irreversible capacity.
  • Methods of forming the tin-nickel alloy film are not specifically restricted but the following methods are used in the present invention by way of examples.
  • tin and nickel are simultaneously deposited by a co-sputtering method.
  • a tin target and a nickel target are separately prepared and co-sputtered for deposition.
  • a single intermetallic compound layer of tin-nickel is formed by the co-sputtering method.
  • the contents of tin and metallic nickel within the single layer can be adjusted by controlling the power of energy sources applied to the tin target and nickel target to be in a predetermined range.
  • tin and metallic nickel are mosaic-sputtered.
  • a tin target and a metallic nickel chips are symmetrically arranged to be sputtered.
  • the composition of tin and nickel can be adjusted by controlling the number of nickel chips.
  • a tin-nickel alloy target is first prepared and then sputtered.
  • the composition of the intermetallic compound thin film of tin and nickel can be adjusted by differing the mixture ratio of tin and metallic nickel in the tin-nickel alloy target.
  • IBAD e-beam evaporation and/or ion beam assisted deposition
  • Tin and metallic nickel powder are first alloyed by a mechanical alloying method to prepare a corresponding evaporation source of a tin-nickel intermetallic compound.
  • the evaporation source is deposited by the e-beam evaporation and/or ion beam assisted deposition (IBAD) to prepare a tin-nickel intermetallic compound thin film.
  • IBAD ion beam assisted deposition
  • accelerated Ar ions are applied to the evaporation source to increase the mobility of metal ions or to change the surface state of the tin-metal film.
  • the composition of the intermetallic compound film of tin-metal can be changed by adjusting the flux of e-beam electrons, and the crystallinity and fine structure of the intermetallic compound film can be adjusted by changing the flux and accelerated voltage of Ar ions.
  • Ni 3 Sn 4 is preferably used as the intermetallic compound of tin and metal in view of structural stability.
  • the intermetallic compound of tin and nickel i.e., Ni 3 Sn 4
  • the tin being an active material of reaction with lithium
  • the nickel not reacting with lithium does not undergo a reaction of forming a compound reacting with lithium ions diffused into the lattice of metal with oxygen ions so that the initial irreversible capacity is almost removed.
  • Ni 3 Sn 4 evaporation source is prepared by mechanically alloying tin and nickel, which will now be explained in more detail.
  • Tin and nickel are mixed in a predetermined molar ratio, pulverized into particles having a predetermined diameter and then heat treated, thereby obtaining the Ni 3 Sn 4 evaporation source.
  • the temperature of heat treatment is closely related to Ni 3 Sn 4 crystalinity, and is preferably in the range of 300 to 550°C. If the heat treatment temperature is less than 300°C, the Ni 3 Sn 4 crystalinity is so weak as not to maintain a Ni 3 Sn 4 crystal structure during charging/discharging cycles, leading to deterioration of cycle characteristics. If the heat treatment temperature is greater than 550°C, grains increase in size during heat treatment, so that grain boundary fraction which act as a host of lithium intercalation/deintercalation is reduced to thus exhibit a decrease in capacity of Ni 3 Sn 4 .
  • the evaporation source is subjected to e-beam evaporation and/or ion-beam assisted deposition (IBAD) to prepare a tin-nickel intermetallic compound (Ni 3 Sn 4 ) film.
  • IBAD ion-beam assisted deposition
  • FIG. 3 is a cross-sectional view of a lithium thin film battery employing an anode thin film according to the present invention.
  • a thin film battery is basically constructed such that a current collector 20 made of platinum is arranged on a substrate 10, a cathode 50, an electrolyte 40 and an anode 30, each being in the form of a film, are sequentially stacked on the current collector 20.
  • the cathode 50 contains lithium composite oxide such as lithium cobalt oxide (LiCoO 2 ), lithium manganese oxide (LiMn 2 O 4 ) or lithium nickel oxide (LiNiO 2 ).
  • the electrolyte 40 consists of Lipon, which is a lithium ion conductive material.
  • the protective film 60 is made of parylene.
  • Lipon represents lithium phosphorus oxynitride.
  • Tin (Sn) and nickel (Ni) powder were mixed in a molar ratio of 4:3 to prepare a tin-nickel intermetallic compound (Ni 3 Sn 4 ) by the following mechanical alloying method.
  • Ni 3 Sn 4 was pre pared by a mechanical alloying method without tin and nickel as starting materials when a mixture of tin and nickel powder were mechanically milled for approximately 10 hours.
  • the Ni 3 Sn 4 crystalinity increased as the heat treatment temperature increased to 350°C and 500°C.
  • a lithium secondary battery was fabricated using metallic lithiums as a counter electrode and a reference electrode and using 1 M LiPF 6 dissolved in a mixed solvent of ethylene carbonate (EC) and diethylcarbonate (DEC) as an electrolyte solution.
  • the cycle characteristics of the prepared lithium secondary battery were evaluated, and the result thereof is shown in FIG. 5 .
  • the cycle characteristics were evaluated by performing charging and discharging at a constant current density of 0.2 mA/cm 2 within the range of measured potential of 0 to 1.2 V.
  • Ni 3 Sn 4 crystalinity became better, the charging/discharging capacity was reduced, leading to remarkable improvement of cycle characteristics. Also, the charging/discharging capacity of Ni 3 Sn 4 powder was proportionate to a volume fraction of the grain boundary of the powder depending on thermal treatment performed after milling. Ni 3 Sn 4 having good crystalinity did not exhibit a decrease in capacity even during lithium intercalation/deintercalation, from which lithium is presumably intercalated/deintercalated into/from the grain boundary of Ni 3 Sn 4 .
  • grains of Ni 3 Sn 4 that is inactive against lithium act as hosts of lithium intercalation/deintercalation, which suppress volume swelling, thereby maintaining good cycle characteristics.
  • FIG. 6 represents an X-ray diffraction analysis based on charging/discharging steps applied to Ni 3 Sn 4 powder prepared by milling tin and nickel powder for approximately 10 hours and thermally treating the same at 500°C for approximately 1 hour, showing the electrochemical change of lithium during intercalation/deintercalation into/from Ni 3 Sn 4 powder.
  • a 0.25 V charging step (b) and a 0.05 V charging step (c) were performed at an initial state (a), lithium intercalation was performed, and then a 1.2 V discharging step (d) was performed, followed by lithium deintercalation.
  • the Ni 3 Sn 4 crystalinity was still maintained. Even after 100 cycles of these steps (e), no change in the diffraction pattern was observed.
  • tin-based intermetallic compounds that have been reported so far, a phase change occurs during lithium intercalation, so that a counter metal relative to tin (Sn) is separated by diffusion of lithium ions, and the lithium ions react with tin (Sn) to form a lithium-tin (Li-Sn) alloy phase.
  • the tin and counter metal formed by the reaction are very small grains and are uniformly distributed, exhibiting improved cycle characteristics relative to tin and the counter metal of tin.
  • the tin-based intermetallic compound undergoes aggregation of tin due to repetition of intercalation and deintercalation of lithium ions, causing severe mechanical damage of active materials due to a change in volume, like in metallic tin, thereby degrading cycle characteristics.
  • Ni 3 Sn 4 structure of the present invention as shown in FIG. 6 , a peak corresponding to tin (Sn) is not observed even during intercalation of lithium, which means that no phase change occurs, unlike in the conventional tin-based intermetallic compounds, but the Ni 3 Sn 4 crystallinity is maintained, thereby greatly improving cycle characteristics.
  • the Ni 3 Sn 4 intermetallic compound as shown in FIG. 5 , has a capacity per weight of approximately 100 mAh/g, which is not suitable to be employed as an anode active material of a bulk-type battery.
  • the Ni 3 Sn 4 intermetallic compound has a large density, i.e., 8.42 g/cm 3 , it can be suitably used as an anode active material in view of good cycle characteristics for a thin film battery in which a capacity per volume is quite an important factor. Also, as shown in FIG.
  • Ni 3 Sn 4 intermetallic compound can be suitably used as the anode material of a thin film battery necessitating high mechanical stability between an electrode and an electrolyte and between an electrode and a current collector.
  • Ni 3 Sn 4 thin film was deposited by e-beam evaporation and ion beam assisted deposition (IBAD) using the Ni 3 Sn 4 powder prepared in Example 1 as an evaporation source.
  • IBAD e-beam evaporation and ion beam assisted deposition
  • FIG. 7 shows X-ray diffraction analysis results of a thin film deposited using the e-beam evaporation and IBAD.
  • Evacuation was performed from an initial vacuum state to 2 ⁇ 10 -6 torr and argon gas was induced to maintain an operating pressure of 2 ⁇ 10 -5 torr.
  • An e-beam acceleration voltage of 5.7 kV and an e-beam current of 20 mA were applied to the Ni 3 Sn 4 powder prepared in the above-described manner for 10 minutes and 20 minutes, respectively for deposition of thin films having thicknesses of 640 ⁇ ( FIG. 7A ) and 920 ⁇ ( FIG. 7B ). Under these conditions, the Ni 3 Sn 4 powder was deposited with an argon ion acceleration voltage of 100 keV and an ion beam current of 20 mA to prepare a thin film having a thickness of 1500 ⁇ .
  • FIG. 8 shows charging/discharging cycle characteristics of the Ni 3 Sn 4 anode film prepared by the above-described process.
  • the plot (a) is for the case of irradiating e-beam for 10 minutes and the plot (b) is for the case of irradiating e-beam for 20 minutes.
  • the crystallinity and cycle characteristic are better than in the case indicated by the plot (a).
  • the cycle characteristic of the Ni 3 Sn 4 anode film is still poorer than that of the Ni 3 Sn 4 powder having good crystallinity.
  • deposition using IBAD can appropriately controls conditions of accelerated ion beam irradiation to increase the mobility and reactivity of atoms while colliding the atoms deposited on the target, thereby preparing a crystalline Ni 3 Sn 4 thin film even at room temperature.
  • Ni 3 Sn 4 powder in which nickel (Ni) and tin (Sn) are stoichiometrically bonded, as an evaporation source, vapor pressures and volatility degrees of nickel and tin are different, which makes it quite difficult to attain a thin film having the same composition as that of the evaporation source.
  • Ni nickel
  • Sn tin
  • accelerated argon (Ar) ions are irradiated onto a substrate simultaneously with the Sn and Ni evaporation sources, thereby increasing the mobility of deposited atoms or changing the surface state of the thin film.
  • the composition of the thin film can be varied by adjusting the flux of e-beam.
  • the crystallinity and fine structure of the deposited thin film can be adjusted by varying the flux and acceleration voltage of Ar ions.
  • FIG. 9 (b) shows the X-ray diffraction analysis result for the thus-prepared thin film
  • FIG. 9 (a) shows the X-ray diffraction analysis result for a Si/SiO 2 substrate.
  • a diffraction peak is observed around a diffraction angle of 28°, from which the thin film is determined as a Ni 3 Sn 2 thin film.
  • FIG. 10 represents charging/discharging cycle characteristics of the Ni 3 Sn 2 anode thin film prepared by the above-described process.
  • the cycle characteristics were evaluated by performing charging and discharging on lithium at a constant current of 30 ⁇ A/cm 2 within the range of measured potential of 0 to 1.2 V.
  • the capacities of the Ni 3 Sn 2 anode thin film are maintained at lower levels, which is because it has a very low electrochemically activity.
  • the Ni 3 Sn 4 thin film can be deposited even at room temperature by varying the composition, crystallinity and fine structure of the thin film such that the flux of e-beams and the flux and acceleration voltage of Ar ions are varied.
  • the cycle characteristics of the anode thin film according to the present invention can be remarkably improved by suppressing dilation and shrinkage of tin during charging/discharging steps. Therefore, use of the anode thin film according to the present invention can greatly improve the chemical, mechanical stability of the interface between an electrode and an electrolyte, thereby preparing a lithium secondary battery having improved life characteristics.

Description

    BACKGROUND OF THE INVENTION 1. Field of the Invention
  • The present invention relates to an anode thin film for lithium secondary battery and a preparation method thereof, and more particularly, to an anode thin film for a lithium secondary battery having a reduced initial irreversible capacity by using an intermetallic compound of tin (Sn) and nickel (Ni) as a material of forming an anode active material layer formed on a current collector, and having improved charging/discharging cycle characteristics by solving the problem of aggregation of tin due to intercalation/deintercalation of lithium.
  • 2. Description of the Related Art
  • It is known that metallic lithium in an organic electrolyte is thermodynamically unstable and is coated with a thin surface layer called a solid electrolyte interface (SEI). The unstable property of the metallic lithium used as an anode-forming material may result in dendrite growth during repeated cycles of charging and discharging, leading to deterioration in stability of battery.
  • A lithium ion battery can secure its stability and can maintain high capacitance characteristics by employing graphite as an anode-forming material. A graphite anode reversibly enables storage and separation of lithium through intercalation of lithium ions. Since the inserted lithium ions are not in the form of metal, factors that may adversely affect the stability of a battery, for example, growth of dendrite, can be prevented.
  • However, graphite anodes have only approximately 10% of an energy density of metallic lithium anodes. Various anode materials including disordered carbon, nitrides or oxides, which exhibit improved capacity compared to graphite, have been proposed for overcoming the problem of small energy density.
  • Various studies Oxide-based anodes exemplified by tin oxides were proposed for the first time by Fuji Photo Film Co., Ltd., in U.S. Patent No. 5,618,640 by Y. Idota et al , and in a paper by Idota et al. entitled "Tin-Based Amorphous Oxide: A High Capacity Lithium-Ion Storage Material", Science, 276 (1997) 1395-1397, and have approximately twice a charge/discharge capacity of graphite-based anodes and are excellent in potential characteristics compared with existing substitutes.
  • Oxide-based anodes consist of oxides of metal that can form lithium alloys, such as tin oxide (SnO or SnO2), lead oxide (PbO) or silicon oxide (SiO). These oxide-based anode-forming materials serve as precursors of anode active materials. Thus, as lithium ions are diffused across the lattice of metal, oxygen ion and metal ion are separated from each other. Also, as intercalated lithium ions react with oxygen ions, separation occurs in the lattice of metal. Active materials capable of charging/discharging are substantially metals separated in the above-described manner, rather than metal oxides.
  • It is also known that lithium can be stored/removed by an alloying reaction between tin and lithium.
  • The oxide-based anodes consisting of oxides, e.g., tin oxide, have good cycle characteristics, compared with lithium alloys, in the following reasons.
  • First, as lithium ions are diffused across the lattice of metal, a metal that can form lithium alloys, e.g., tin, is separated. However, the separated metal is very small in size, the mechanical loss of an active material, due to a change in volume, can be minimized.
  • Second, since, during initial stage of lithium storage, lithium oxide (Li2O), which is a product based on the reaction between the lithium produced simultaneously with separated metal during initial storage of lithium, and the oxygen ions, is evenly dispersed, damage of the active material due to a change in volume can be suppressed.
  • However, the oxide-based anode exhibits a relatively high initial irreversible capacity due to formation of lithium oxide, which is necessarily generated during the first charging/discharging cycle. Accordingly, an excess amount of a cathode active material is required, which is impediment to practical use.
  • In order to reduce the initial irreversible capacity while maintaining high capacity and good cycle characteristics of an oxide-based anode, there have been proposed methods in which an intermetallic compound or nano-sized metal powder is employed. The methods in which an intermetallic compound is employed are disclosed in U.S. Patent No. 6,203,944 by Robert L. Turner et al , entitled "Electrode for a lithium battery," papers entitled "Mechanically Alloyed Sn-Fe(-C) Powders as Anode Materials for Li-Ion Batteries," by Mao et al., J. Electrochem. Soc., 146 (2) (1999) 405-413, "The Reaction of Lithium with Sn-Mn-C Intermetallics Prepared by Mechanical Alloying," by Beaulieu et al, J. Electrochem. Soc., 147 (9) (2000) 3237-3241, and "LixCu6Sn5 (0<x<13): An Intermetallic Insertion Electrode for Rechargeable Lithium Batteries," by Kepler et al., Electrochem. Solid-State Lett., 2 (7) (1999) 307-309. The methods in which nano-sized metal powder is employed are disclosed in papers entitled "Sub-Microcrystalline Sn and Sn-SnSb powders as Lithium Storage Materials for Lithium Ion Batteries," by Yang et al., Electrochem. Solid-State Lett., 2 (4) (1999) 161-163, and "Ultrafine Sn and SnSb0.14 Powders for Lithium Storage Materials in Lithium-Ion Batteries," by Yang et al., J. Electrochem. Soc., 146 (11) (1999) 4009-4013.
  • The former methods will now be described in more detail. A tin-based intermetallic compound, for example, Sn2Fe or Cu6Sn5, consists of an intermetallic compound of a metal which does not form a lithium alloy and a metal which is reactive with lithium. Also, since the tin-based intermetallic compound does not undergo irreversible reaction, e.g., formation of lithium oxide (Li2O) due to diffusion of lithium ions into the lattice of metal, unlike tin oxide, initial irreversible capacity can be reduced.
  • However, the tin-based intermetallic compound causes aggregation of tin due to repeated intercalation/deintercalation of lithium ions, which aggravates the mechanical damage of an active material depending on a change in volume, like metallic tin, resulting in considerable deterioration of cycle characteristics.
  • To solve the above-described problems, an attempt to use a composite material of an active-phase material enabling intercalation/deintercalation of lithium and an inactive-phase material non-reactive with lithium, prepared by a mechanical alloying method, as an anode forming material, has been made.
  • Detailed examples of the composite material include a composite material consisting of Sn2Fe as an active-phase material and SnFe3C as an inactive-phase material. While such a composite material has a fine structure, improved cycle characteristics due to addition of inactive-phase material, and an increased energy density per volume, its energy density per weight is very small, i.e., less than 200 mAh/g.
  • As shown in FIG. 1, a lithium-tin alloy (Li4.4Sn) has a relatively low operating voltage with respect to a lithium electrode, i.e., 0.7 V or less, and has an energy density per unit weight of approximately 790 mAh/g, which is higher than that of a lithium-graphite compound (LiC6) having an energy density of 342 mAh/g.
  • In the lithium-tin alloy enabling intercalation/deintercalation of lithium, aggregation of tin, which is due to intercalation/deintercalation of lithium, and a severe change in volume, cause cracks on the surface of and within tin, which leads to electrical disconnection with a current collector, thereby deteriorating cycle characteristics, which is confirmed in FIG. 2.
  • Referring to FIG. 2, when an anode of lithium-tin alloy film is charged/discharged with a constant current of 50 µA/cm2 up to 0 to 1.2 V, the initial charge capacity thereof began to sharply decrease after repetition of 5 cycles until it vanishes after repetition of 20 cycles, that is, the cycle life is deteriorated.
  • EP 1 122 802 A1 discloses a non-aqueous electrolyte secondary battery comprising a negative electrode including, as an active material, a solid solution of LixM1 yM2, where M1 and M2 represent specific metals, and x and y represent specific amounts of Li and M1, respectively. As far as Ni and Sn are considered for M1 and M2, the compositions NiSn, Ni2Sn, and Ni3Sn are proposed. The solid solution typically shows an average particle size of 0.5 µm to 2.3 µm, and an average crystal grain size of 0.05 µm to 0.13 µm. Further, EP 1 043 789 A1 discloses for such negative electrode compound to have at least two phases of different composition. For example, an alloy composition NiSn is proposed to consist of an Ni3Sn4 phase and an Ni3Sn phase as well as an Sn(2) phase. The thickness of a practical negative electrode sheet is said to be about 80 µm. Similar electrode compositions for a lithium ion battery with particle sizes from about 2 µm to about 30 µm and crystalline grain sizes of no more than about 20 nm are disclosed in WO 01/48840 A1 , where the particles have a microstructure including a plurality of electrochemically inactive, nanometer-sized crystalline grains separated by electrochemically active non-crystalline regions.
  • US 5,360,684 discloses an electrochemical cell having a specific lamination structure including a lithium negative electrode with a typical thickness of 20 µm and a positive electrode with a typical thickness of 40 µm.
  • SUMMARY OF THE INVENTION
  • To solve the above-described problems, it is a first object of the present invention to provide an anode thin film for a lithium secondary battery, which can solve the problem of aggregation of tin due to intercalation/deinterealation of lithium.
  • It is a second object of the present invention to provide a manufacturing method of the anode thin film.
  • It is a third object of the present invention to provide a lithium secondary battery having improved charging/discharging characteristics by employing the anode thin film.
  • To accomplish the above and other objects, an anode thin film for a lithium secondary battery according to an embodiment of the present invention includes a current collector and an anode active material layer formed thereon, wherein the anode active material layer contains an intermetallic compound of Ni3Sn4.
  • According to another aspect of the present invention, a method of preparing such anode thin film for a lithium secondary battery includes mosaic-sputtering tin (Sn) and metallic nickel (Ni), co-sputtering tin (Sn) and metallic nickel (Ni) and sputtering single target or target containing tin (Sn) and metallic nickel (Ni).
  • According to another aspect of the present invention, a method of preparing such anode thin film for a lithium secondary battery includes the steps of forming an intermetallic compound evaporation source of tin (Sn) and metallic nickel (Ni) by a mechanical alloying method and depositing the intermetallic compound evaporation source by at least selected from the group consisting of e-beam evaporation and ion beam assisted deposition (IBAD).
  • According to yet another aspect of the present invention, a lithium secondary battery employs the anode thin film. The lithium secondary battery is preferably a lithium thin film battery.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • The above objects and advantages of the present invention will become more apparent by describing in detail preferred embodiments thereof with reference to the attached drawings in which:
    • FIG. 1 is a charging/discharging cycle voltage curve of a conventional lithium-tin alloy;
    • FIG. 2 is a graph showing the cycle characteristic of the conventional anode of a lithium-tin alloy film;
    • FIG. 3 is a cross-sectional view of a lithium thin film battery employing an anode thin film according to the present invention;
    • FIG. 4 represents an X-ray diffraction analysis of Ni3Sn4 prepared by Example 1 of the present invention;
    • FIG. 5 represents charging/discharging cycle characteristics of a lithium secondary battery employing Ni3Sn4 prepared by Example 1 of the present invention;
    • FIG. 6 represents an X-ray diffraction analysis of Ni3Sn4 at (a) initial state, (b) 0.25 V charging state, (c) 0.05 V charging state, (d) 1.2 V discharging state, and (e) after 100 cycles, in the lithium secondary battery employing Ni3Sn4 prepared by Example 1 of the present invention;
    • FIG. 7 represents an X-ray diffraction analysis of a Ni3Sn4 anode thin film prepared by Example 2 of the present invention;
    • FIG. 8 represents charging/discharging cycle characteristics of a lithium secondary battery employing the Ni3Sn4 anode thin film prepared by Example 2 of the present invention;
    • FIG. 9 represents an X-ray diffraction analysis of the Ni3Sn4 anode thin film prepared by Example 2 of the present invention; and
    • FIG. 10 represents charging/discharging cycle characteristics of the Ni3Sn4 anode thin film prepared by Example 2 of the present invention.
    DETAILED DESCRIPTION OF THE INVENTION
  • The present invention is directed to improvement in cycle characteristics by employing an intermetallic compound of tin (Sn) and nickel (Ni) in order to solve an inherent problem of tin, that is, in order to suppress a stress due to volumetric expansion of tin, thereby improving the structural stability to improve cycle characteristics.
  • Unlike the conventional lithium-tin alloy, the intermetallic compound of tin (Sn) and a nickel (Ni) metal, that is, Ni3Sn4, the tin (Sn) being an active material of reaction with lithium (Li) and the nickel (Ni) metal not reacting with Li, does not undergo a reaction of forming a compound with Li ions diffused into a grid with oxygen ions contained in oxide, thereby almost removing the initial irreversible capacity.
  • Methods of forming the tin-nickel alloy film are not specifically restricted but the following methods are used in the present invention by way of examples.
  • First, tin and nickel are simultaneously deposited by a co-sputtering method.
  • According to this method, a tin target and a nickel target are separately prepared and co-sputtered for deposition. In such a manner, a single intermetallic compound layer of tin-nickel is formed by the co-sputtering method. The contents of tin and metallic nickel within the single layer can be adjusted by controlling the power of energy sources applied to the tin target and nickel target to be in a predetermined range.
  • Second, tin and metallic nickel are mosaic-sputtered. According to this method, a tin target and a metallic nickel chips are symmetrically arranged to be sputtered. Here, the composition of tin and nickel can be adjusted by controlling the number of nickel chips.
  • Third, a tin-nickel alloy target is first prepared and then sputtered. Here, the composition of the intermetallic compound thin film of tin and nickel can be adjusted by differing the mixture ratio of tin and metallic nickel in the tin-nickel alloy target.
  • Fourth, e-beam evaporation and/or ion beam assisted deposition (IBAD) may be used.
  • Tin and metallic nickel powder are first alloyed by a mechanical alloying method to prepare a corresponding evaporation source of a tin-nickel intermetallic compound.
  • Thereafter, the evaporation source is deposited by the e-beam evaporation and/or ion beam assisted deposition (IBAD) to prepare a tin-nickel intermetallic compound thin film. Here, accelerated Ar ions are applied to the evaporation source to increase the mobility of metal ions or to change the surface state of the tin-metal film. Also, the composition of the intermetallic compound film of tin-metal can be changed by adjusting the flux of e-beam electrons, and the crystallinity and fine structure of the intermetallic compound film can be adjusted by changing the flux and accelerated voltage of Ar ions.
  • Ni3Sn4 is preferably used as the intermetallic compound of tin and metal in view of structural stability. Unlike conventional lithium-tin alloy, the intermetallic compound of tin and nickel, i.e., Ni3Sn4, the tin being an active material of reaction with lithium, and the nickel not reacting with lithium, does not undergo a reaction of forming a compound reacting with lithium ions diffused into the lattice of metal with oxygen ions so that the initial irreversible capacity is almost removed.
  • The method of preparing a thin film using the tin-nickel intermetallic compound Ni3Sn4 will now be described.
  • First, a Ni3Sn4 evaporation source is prepared by mechanically alloying tin and nickel, which will now be explained in more detail.
  • Tin and nickel are mixed in a predetermined molar ratio, pulverized into particles having a predetermined diameter and then heat treated, thereby obtaining the Ni3Sn4 evaporation source. Here, the temperature of heat treatment is closely related to Ni3Sn4 crystalinity, and is preferably in the range of 300 to 550°C. If the heat treatment temperature is less than 300°C, the Ni3Sn4 crystalinity is so weak as not to maintain a Ni3Sn4 crystal structure during charging/discharging cycles, leading to deterioration of cycle characteristics. If the heat treatment temperature is greater than 550°C, grains increase in size during heat treatment, so that grain boundary fraction which act as a host of lithium intercalation/deintercalation is reduced to thus exhibit a decrease in capacity of Ni3Sn4.
  • Thereafter, the evaporation source is subjected to e-beam evaporation and/or ion-beam assisted deposition (IBAD) to prepare a tin-nickel intermetallic compound (Ni3Sn4) film.
  • FIG. 3 is a cross-sectional view of a lithium thin film battery employing an anode thin film according to the present invention. Referring to FIG. 3, a thin film battery is basically constructed such that a current collector 20 made of platinum is arranged on a substrate 10, a cathode 50, an electrolyte 40 and an anode 30, each being in the form of a film, are sequentially stacked on the current collector 20. A protective film 60 for protecting the thin film battery by shielding the same from outside, is deposited on the anode 30.
  • In the thin film battery having the aforementioned configuration, the cathode 50 contains lithium composite oxide such as lithium cobalt oxide (LiCoO2), lithium manganese oxide (LiMn2O4) or lithium nickel oxide (LiNiO2). The electrolyte 40 consists of Lipon, which is a lithium ion conductive material. The protective film 60 is made of parylene. Here, Lipon represents lithium phosphorus oxynitride.
  • The present invention will now be described in more detail through the following examples, but not limited thereto.
  • Example 1
  • Tin (Sn) and nickel (Ni) powder were mixed in a molar ratio of 4:3 to prepare a tin-nickel intermetallic compound (Ni3Sn4) by the following mechanical alloying method.
  • That is to say, after tin (Sn) and nickel (Ni) powders were weighed in a molar ratio of 4:3, tin (Sn) and nickel (Ni) were mixed sufficiently using an agate mortar and ball-milled at approximately 750 rpm using an oscillation-type ball mill for approximately 10 hours. After ball-milling, the resultant was thermally treated at 350°C and 500°C for approximately 1 hour to prepare a tin-nickel intermetallic compound (Ni3Sn4). The X-ray diffraction analysis result of the prepared tin-nickel intermetallic compound (Ni3Sn4) is shown in FIG. 4. Referring to FIG. 4A, it was confirmed that only Ni3Sn4 was prepared by a mechanical alloying method without tin and nickel as starting materials when a mixture of tin and nickel powder were mechanically milled for approximately 10 hours. As shown in FIGS. 4B and 4C, the Ni3Sn4 crystalinity increased as the heat treatment temperature increased to 350°C and 500°C.
  • In order to evaluate electrochemical properties of Ni3Sn4 compounds prepared by the above-described procedure, a lithium secondary battery was fabricated using metallic lithiums as a counter electrode and a reference electrode and using 1 M LiPF6 dissolved in a mixed solvent of ethylene carbonate (EC) and diethylcarbonate (DEC) as an electrolyte solution. The cycle characteristics of the prepared lithium secondary battery were evaluated, and the result thereof is shown in FIG. 5. Here, the cycle characteristics were evaluated by performing charging and discharging at a constant current density of 0.2 mA/cm2 within the range of measured potential of 0 to 1.2 V.
  • Referring to FIG. 5, as the Ni3Sn4crystalinity became better, the charging/discharging capacity was reduced, leading to remarkable improvement of cycle characteristics. Also, the charging/discharging capacity of Ni3Sn4 powder was proportionate to a volume fraction of the grain boundary of the powder depending on thermal treatment performed after milling. Ni3Sn4 having good crystalinity did not exhibit a decrease in capacity even during lithium intercalation/deintercalation, from which lithium is presumably intercalated/deintercalated into/from the grain boundary of Ni3Sn4. Here, grains of Ni3Sn4 that is inactive against lithium act as hosts of lithium intercalation/deintercalation, which suppress volume swelling, thereby maintaining good cycle characteristics.
  • FIG. 6 represents an X-ray diffraction analysis based on charging/discharging steps applied to Ni3Sn4 powder prepared by milling tin and nickel powder for approximately 10 hours and thermally treating the same at 500°C for approximately 1 hour, showing the electrochemical change of lithium during intercalation/deintercalation into/from Ni3Sn4 powder.
  • Referring to FIG. 6, a 0.25 V charging step (b) and a 0.05 V charging step (c) were performed at an initial state (a), lithium intercalation was performed, and then a 1.2 V discharging step (d) was performed, followed by lithium deintercalation. The Ni3Sn4 crystalinity was still maintained. Even after 100 cycles of these steps (e), no change in the diffraction pattern was observed.
  • In known tin-based intermetallic compounds that have been reported so far, a phase change occurs during lithium intercalation, so that a counter metal relative to tin (Sn) is separated by diffusion of lithium ions, and the lithium ions react with tin (Sn) to form a lithium-tin (Li-Sn) alloy phase. The tin and counter metal formed by the reaction are very small grains and are uniformly distributed, exhibiting improved cycle characteristics relative to tin and the counter metal of tin. However, the tin-based intermetallic compound undergoes aggregation of tin due to repetition of intercalation and deintercalation of lithium ions, causing severe mechanical damage of active materials due to a change in volume, like in metallic tin, thereby degrading cycle characteristics.
  • On the other hand, in the Ni3Sn4 structure of the present invention as shown in FIG. 6, a peak corresponding to tin (Sn) is not observed even during intercalation of lithium, which means that no phase change occurs, unlike in the conventional tin-based intermetallic compounds, but the Ni3Sn4 crystallinity is maintained, thereby greatly improving cycle characteristics.
  • The Ni3Sn4 intermetallic compound, as shown in FIG. 5, has a capacity per weight of approximately 100 mAh/g, which is not suitable to be employed as an anode active material of a bulk-type battery. However, since the Ni3Sn4 intermetallic compound has a large density, i.e., 8.42 g/cm3, it can be suitably used as an anode active material in view of good cycle characteristics for a thin film battery in which a capacity per volume is quite an important factor. Also, as shown in FIG. 3, since there is little change in lattice constant due to lithium intercalation/deintercalation, it is presumed that a change in volume is not so big during lithium intercalation, which means that the Ni3Sn4 intermetallic compound can be suitably used as the anode material of a thin film battery necessitating high mechanical stability between an electrode and an electrolyte and between an electrode and a current collector.
  • Example 2
  • A Ni3Sn4 thin film was deposited by e-beam evaporation and ion beam assisted deposition (IBAD) using the Ni3Sn4 powder prepared in Example 1 as an evaporation source.
  • FIG. 7 shows X-ray diffraction analysis results of a thin film deposited using the e-beam evaporation and IBAD. Evacuation was performed from an initial vacuum state to 2×10-6 torr and argon gas was induced to maintain an operating pressure of 2×10-5 torr. An e-beam acceleration voltage of 5.7 kV and an e-beam current of 20 mA were applied to the Ni3Sn4 powder prepared in the above-described manner for 10 minutes and 20 minutes, respectively for deposition of thin films having thicknesses of 640 Å (FIG. 7A) and 920 Å (FIG. 7B). Under these conditions, the Ni3Sn4 powder was deposited with an argon ion acceleration voltage of 100 keV and an ion beam current of 20 mA to prepare a thin film having a thickness of 1500 Å.
  • Referring to FIG. 7, when the time of deposition by e-beam evaporation is increased or ion beams are irradiated onto a substrate, a diffraction peak is observed around a diffraction angle of 30°, which is presumably derived from NiSn which is a metastable phase.
  • FIG. 8 shows charging/discharging cycle characteristics of the Ni3Sn4 anode film prepared by the above-described process.
  • Referring to FIG. 8, the plot (a) is for the case of irradiating e-beam for 10 minutes and the plot (b) is for the case of irradiating e-beam for 20 minutes. In the case indicated by the plot (b), the crystallinity and cycle characteristic are better than in the case indicated by the plot (a). However, the cycle characteristic of the Ni3Sn4 anode film is still poorer than that of the Ni3Sn4 powder having good crystallinity. These results show that use of the Ni3Sn4 powder, in which nickel (Ni) and tin (Sn) are stoichiometrically bonded, as an evaporation source, makes it difficult to control the composition of the deposited thin film.
  • On the other hand, as shown in FIG. 7(c), deposition using IBAD can appropriately controls conditions of accelerated ion beam irradiation to increase the mobility and reactivity of atoms while colliding the atoms deposited on the target, thereby preparing a crystalline Ni3Sn4 thin film even at room temperature.
  • As described above, in the case of using Ni3Sn4 powder, in which nickel (Ni) and tin (Sn) are stoichiometrically bonded, as an evaporation source, vapor pressures and volatility degrees of nickel and tin are different, which makes it quite difficult to attain a thin film having the same composition as that of the evaporation source. To solve this problem, there has been made an attempt to facilitate control of the compositions of tin and nickel by co-fusing e-beams using tin and nickel as evaporation sources, respectively. Here, accelerated argon (Ar) ions are irradiated onto a substrate simultaneously with the Sn and Ni evaporation sources, thereby increasing the mobility of deposited atoms or changing the surface state of the thin film. The composition of the thin film can be varied by adjusting the flux of e-beam. The crystallinity and fine structure of the deposited thin film can be adjusted by varying the flux and acceleration voltage of Ar ions.
  • First, an initial vacuum state is turned into an evacuated state up to 2×10-6 torr and argon gas was induced to maintain an operating pressure of 2×10-5 torr. Thereafter, under the condition of an e-beam acceleration voltage of 5.7 kV, e-beam currents of 110 mA and 75 mA were applied to tin and nickel, respectively, for deposition of a thin film having a thickness of 950 Å. FIG. 9 (b) shows the X-ray diffraction analysis result for the thus-prepared thin film, whereas FIG. 9 (a) shows the X-ray diffraction analysis result for a Si/SiO2 substrate. As shown in FIG. 9 (b), a diffraction peak is observed around a diffraction angle of 28°, from which the thin film is determined as a Ni3Sn2 thin film.
  • FIG. 10 represents charging/discharging cycle characteristics of the Ni3Sn2 anode thin film prepared by the above-described process. Here, the cycle characteristics were evaluated by performing charging and discharging on lithium at a constant current of 30 µA/cm2 within the range of measured potential of 0 to 1.2 V.
  • As shown in FIG. 10, the capacities of the Ni3Sn2 anode thin film are maintained at lower levels, which is because it has a very low electrochemically activity.
  • However, as described above, the Ni3Sn4 thin film can be deposited even at room temperature by varying the composition, crystallinity and fine structure of the thin film such that the flux of e-beams and the flux and acceleration voltage of Ar ions are varied.
  • The cycle characteristics of the anode thin film according to the present invention can be remarkably improved by suppressing dilation and shrinkage of tin during charging/discharging steps. Therefore, use of the anode thin film according to the present invention can greatly improve the chemical, mechanical stability of the interface between an electrode and an electrolyte, thereby preparing a lithium secondary battery having improved life characteristics.

Claims (8)

  1. An anode thin film for a lithium secondary battery having a current collector and an anode active material layer formed thereon,
    characterized in that
    the anode active material layer contains a thin film intermetallic compound of Ni3Sn4.
  2. The anode thin film of claim 1, wherein the thin film intermetallic compound is deposited from an Ni3Sn4 powder material.
  3. A method of preparing an anode thin film of claim 1 or 2 by mosaic-sputtering tin (Sn) and metallic nickel (Ni).
  4. A method of preparing an anode thin film of claim 1 or 2 by co-sputtering tin (Sn) and metallic nickel (Ni).
  5. A method of preparing an anode thin film of claim 1 or 2 by sputtering a single target containing tin (Sn) and metallic nickel (Ni).
  6. A method of preparing an anode thin film of claim 1 or 2 by forming an intermetallic compound evaporation source of tin (Sn) and metallic nickel (Ni) by a mechanical alloying method and depositing the intermetallic compound evaporation source by a deposition method selected from the group consisting of at least e-beam evaporation and ion beam assisted deposition (IBAD).
  7. A lithium secondary battery comprising an anode thin film of claim 1 or 2.
  8. The lithium secondary battery of claim 7, wherein the battery is a thin film battery.
EP02000438.8A 2001-08-28 2002-01-08 Anode thin film for lithium secondary battery and preparation method thereof Expired - Lifetime EP1289033B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR10-2001-0052111A KR100416094B1 (en) 2001-08-28 2001-08-28 Anode thin film for Lithium secondary battery and preparation method thereof
KR2001052111 2001-08-28

Publications (3)

Publication Number Publication Date
EP1289033A2 EP1289033A2 (en) 2003-03-05
EP1289033A3 EP1289033A3 (en) 2005-03-16
EP1289033B1 true EP1289033B1 (en) 2013-07-10

Family

ID=19713644

Family Applications (1)

Application Number Title Priority Date Filing Date
EP02000438.8A Expired - Lifetime EP1289033B1 (en) 2001-08-28 2002-01-08 Anode thin film for lithium secondary battery and preparation method thereof

Country Status (4)

Country Link
US (1) US7052801B2 (en)
EP (1) EP1289033B1 (en)
JP (1) JP3609377B2 (en)
KR (1) KR100416094B1 (en)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6942944B2 (en) * 2000-02-29 2005-09-13 Illinois Institute Of Technology Battery system thermal management
US8273474B2 (en) * 2000-02-29 2012-09-25 Illinois Institute Of Technology Battery system thermal management
KR100448519B1 (en) * 2002-09-23 2004-09-13 한국과학기술연구원 Method for manufacturing porous electrode and thin film electrolyte for micro electrochemical device
US20090029264A1 (en) * 2005-02-02 2009-01-29 Geomatec Co., Ltd. Thin-Film Solid Secondary Cell
KR100764619B1 (en) * 2005-04-04 2007-10-08 주식회사 엘지화학 Lithium Secondary Battery Containing Silicon-based or Tin-based Anode Active Material
KR100742227B1 (en) * 2005-04-12 2007-07-24 주식회사 엘지화학 Lithium Secondary Battery Containing Silicon-based or Tin-based Anode Active Material
JP5200339B2 (en) * 2006-06-16 2013-06-05 パナソニック株式会社 Nonaqueous electrolyte secondary battery
JP5489859B2 (en) * 2009-05-21 2014-05-14 株式会社半導体エネルギー研究所 Conductive film and method for manufacturing conductive film
JP2011014884A (en) * 2009-06-05 2011-01-20 Semiconductor Energy Lab Co Ltd Photoelectric conversion device
KR101156532B1 (en) * 2009-11-27 2012-06-20 삼성에스디아이 주식회사 Negative electrode for lithium battery and lithium battery comprising the same
CN102832377A (en) * 2012-08-17 2012-12-19 华南理工大学 Tin-amorphous nickel titanium composite film cathode material and preparation method and application thereof
CN103268933B (en) * 2013-05-06 2015-01-28 华南理工大学 Al-Sn film negative electrode and preparation method thereof
GB201400276D0 (en) * 2014-01-08 2014-02-26 Ilika Technologies Ltd Vapour deposition method for fabricating lithium-containing thin film layered structures
US10547040B2 (en) * 2016-04-14 2020-01-28 Applied Materials, Inc. Energy storage device having an interlayer between electrode and electrolyte layer
GB2590398B (en) * 2019-12-16 2022-08-31 Dyson Technology Ltd Methods of making anode architectures

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4094761A (en) * 1977-07-25 1978-06-13 Motorola, Inc. Magnetion sputtering of ferromagnetic material
JPS60124357A (en) * 1983-12-08 1985-07-03 Matsushita Electric Ind Co Ltd Negative electrode of nonaqueous electrolyte secondary battery
JP3134340B2 (en) * 1991-04-05 2001-02-13 東ソー株式会社 Sputtering target
US5618640A (en) * 1993-10-22 1997-04-08 Fuji Photo Film Co., Ltd. Nonaqueous secondary battery
JP3359164B2 (en) * 1994-10-19 2002-12-24 キヤノン株式会社 Rechargeable battery
JP3644106B2 (en) * 1995-12-26 2005-04-27 宇部興産株式会社 Non-aqueous secondary battery
JP4142753B2 (en) * 1996-12-26 2008-09-03 株式会社東芝 Sputtering target, sputtering apparatus, semiconductor device and manufacturing method thereof
JPH1186854A (en) * 1997-09-11 1999-03-30 Hitachi Ltd Lithium secondary battery
US6203944B1 (en) * 1998-03-26 2001-03-20 3M Innovative Properties Company Electrode for a lithium battery
WO2000024070A1 (en) * 1998-10-22 2000-04-27 Matsushita Electric Industrial Co., Ltd. Secondary cell having non-aqueous electrolyte
KR100426095B1 (en) * 1999-07-01 2004-04-06 마쯔시다덴기산교 가부시키가이샤 Non-aqueous electrolyte secondary cell
JP3103356B1 (en) * 1999-09-28 2000-10-30 株式会社サムスン横浜研究所 Negative electrode material for lithium secondary battery, electrode for lithium secondary battery, method for producing lithium secondary battery and negative electrode material for lithium secondary battery
WO2001048840A1 (en) * 1999-12-28 2001-07-05 3M Innovative Properties Company Grain boundary materials as electrodes for lithium ion cells
JP2001256968A (en) 2000-03-13 2001-09-21 Mitsui Mining & Smelting Co Ltd Anode material for nonaqueous electrolyte secondary battery and manufacturing method thereof
JP2001256967A (en) * 2000-03-13 2001-09-21 Mitsui Mining & Smelting Co Ltd Anode material for nonaqueous electrolyte secondary battery and manufacturing method thereof
JP3388408B2 (en) * 2000-10-24 2003-03-24 鈴鹿工業高等専門学校長 Manufacturing method of tin-nickel alloy film

Also Published As

Publication number Publication date
KR100416094B1 (en) 2004-01-24
KR20030018399A (en) 2003-03-06
US20030044682A1 (en) 2003-03-06
US7052801B2 (en) 2006-05-30
EP1289033A3 (en) 2005-03-16
JP2003077464A (en) 2003-03-14
EP1289033A2 (en) 2003-03-05
JP3609377B2 (en) 2005-01-12

Similar Documents

Publication Publication Date Title
EP1207566B1 (en) Anode thin film for lithium secondary battery
EP1099265B1 (en) Electrode material and compositions including same
US7316867B2 (en) Method for manufacturing a multi-layered thin film for use as an anode in a lithium secondary battery
EP1635417B1 (en) Lithium secondary battery and method for producing same
KR101020909B1 (en) Negative electrode for lithium secondary battery, method for producing same, and lithium secondary battery comprising such negative electrode for lithium secondary battery
EP1633013B1 (en) Lithium secondary battery and method for producing same
US6887511B1 (en) Method for preparing electrode material for lithium battery
US20040241548A1 (en) Negative electrode active material and non-aqueous electrolyte rechargeable battery using the same
EP1289033B1 (en) Anode thin film for lithium secondary battery and preparation method thereof
JP2006511907A (en) High energy density High power density electrochemical cell
Uzakbaiuly et al. Physical vapor deposition of cathode materials for all solid-state Li ion batteries: a review
WO2005076389A9 (en) Self-contained, alloy type, thin film anodes for lithium-ion batteries
EP1959513B1 (en) Composite anode active material,method of preparing the same,and anode and lithium battery containing the material
KR101124492B1 (en) Method of preparing positine active material for lithium battery
JP2002289177A (en) Lithium secondary battery and electrode for it
KR20180039039A (en) Electrode active material, preparation method thereof, and electrode and lithium battery containing the same
JP2002298834A (en) Lithium secondary battery and positive electrode for the lithium secondary battery
CN111430720B (en) Electrode protection layer and preparation method thereof, electrode and lithium battery
JP3869609B2 (en) Method for producing electrode for lithium secondary battery
KR20080070492A (en) Composite anode active material, method of preparing the same, and anode and lithium battery containing the material
JP3935729B2 (en) Electrode for lithium secondary battery
JPH07296796A (en) Negative electrode for lithium secondary battery, and lithium secondary battery
KR20060067459A (en) Silicon containing multi-layered thin film electrodes for lithium secondary battery and preparation thereof
JP2005268016A (en) Manufacturing method of lithium secondary battery
KR20140073614A (en) Anode active material, lithium secondary battery employing the same, and preparing method thereof

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

AX Request for extension of the european patent

Extension state: AL LT LV MK RO SI

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

AX Request for extension of the european patent

Extension state: AL LT LV MK RO SI

17P Request for examination filed

Effective date: 20050915

AKX Designation fees paid

Designated state(s): DE FR GB

17Q First examination report despatched

Effective date: 20101210

RIC1 Information provided on ipc code assigned before grant

Ipc: H01M 10/052 20100101ALI20121126BHEP

Ipc: C22C 13/00 20060101ALI20121126BHEP

Ipc: H01M 4/04 20060101ALI20121126BHEP

Ipc: C23C 14/46 20060101ALI20121126BHEP

Ipc: C23C 14/34 20060101ALI20121126BHEP

Ipc: H01M 4/38 20060101AFI20121126BHEP

Ipc: C23C 14/16 20060101ALI20121126BHEP

Ipc: C23C 14/30 20060101ALI20121126BHEP

Ipc: H01M 4/1395 20100101ALI20121126BHEP

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): DE FR GB

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 60245191

Country of ref document: DE

Effective date: 20130905

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed

Effective date: 20140411

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 60245191

Country of ref document: DE

Effective date: 20140411

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 15

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 16

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 17

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20191231

Year of fee payment: 19

Ref country code: GB

Payment date: 20200102

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20200113

Year of fee payment: 19

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 60245191

Country of ref document: DE

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20210108

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20210131

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20210108

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20210803